CN107519775A - A kind of emulsifier unit - Google Patents
A kind of emulsifier unit Download PDFInfo
- Publication number
- CN107519775A CN107519775A CN201710825953.5A CN201710825953A CN107519775A CN 107519775 A CN107519775 A CN 107519775A CN 201710825953 A CN201710825953 A CN 201710825953A CN 107519775 A CN107519775 A CN 107519775A
- Authority
- CN
- China
- Prior art keywords
- fluid
- fluid passage
- air deflector
- passage
- emulsifier unit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
- B01F23/4105—Methods of emulsifying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/41—Emulsifying
- B01F23/414—Emulsifying characterised by the internal structure of the emulsion
- B01F23/4145—Emulsions of oils, e.g. fuel, and water
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/30—Micromixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/30—Micromixers
- B01F33/301—Micromixers using specific means for arranging the streams to be mixed, e.g. channel geometries or dispositions
- B01F33/3017—Mixing chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/48—Mixing water in water-taps with other ingredients, e.g. air, detergents or disinfectants
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
Abstract
The present invention relates to micro-mixer technology, proposes a kind of emulsifier unit, including：First fluid passage (13) for high viscosity fluid；Second fluid passage (23) for low viscosity fluid；First fluid air deflector (12), the fluid inlet end of first fluid passage (13) are connected to first fluid air deflector (12)；Second fluid air deflector (22), the fluid inlet end of second fluid passage (23) are connected to second fluid air deflector (22)；Water conservancy diversion header (3), the first fluid outlet (11) of first fluid passage (13) and the second fluid outlet (21) of second fluid passage (23) are commonly connected to water conservancy diversion header (3).The emulsifier unit of the present invention reduces the pressure drop of oil phase, improves mixed effect.
Description
Technical field
The present invention relates to the micro-structural emulsifying technology of chemical field, is applied to high viscosity oil phase more particularly, to one kind
The emulsifier unit of fluid.
Background technology
Micro-structured reactor typically has equivalent straight due to having good Heat and Mass Transfer Characteristics with very big specific surface area
Footpath is less than 500 μm of microstructure.According to function, microreactor, micro heat exchanger, micro-mixer etc. can be broadly divided into.
Emulsification can be realized by micro-mixer.Water-oil phase is emulsified by micro-mixer.Existing micro-mixer is most
It is that situation about being more or less the same based on two kinds of fluid viscosity coefficients is designed.When being emulsified using micro-mixer, if oil phase viscosity
Very high, then most energy expenditures do not dissipate in passage in hybrid chamber.For micro-emulsifier, pressure drop is emulsification
Power resources.Therefore emulsifying effectiveness is undesirable.Even oil phase viscosity is high does not provide enough energy to conventional fluid machinery
To overcome flow resistance.
The content of the invention
When mutually being emulsified at present using heavy oil by micro-mixer, oil phase passage, which has very big flowing, to be damaged
Lose, present invention is mainly applied to the field emulsified by micro-mixer, it is therefore an objective to reduce oil phase by reactor microchannel
During energy loss.
The present invention proposes a kind of emulsifier unit, including：
A kind of emulsifier unit, including：First fluid passage for high viscosity fluid；Second for low viscosity fluid
Body passage；First fluid air deflector, the fluid inlet end of first fluid passage are connected to first fluid air deflector；Second fluid is led
Device is flowed, the fluid inlet end of second fluid passage is connected to second fluid air deflector；Water conservancy diversion header, the first of first fluid passage
The outlet of the second fluid of fluid issuing and second fluid passage is commonly connected to water conservancy diversion header.
The technique effect of the emulsifier unit of the present invention includes：
1. the present invention is suitable for high viscosity fluid.And it is applied to production-scale amplification.
2. the present invention in the case of water has very big viscosity, is improved proposition in terms of MCA for oil phase.So
In the processing and manufacturing of microchannel, microchannel is improved so that oily microchannel is shorter than the microchannel of water, and advantage of the invention exists
In oil phase microchannel can be worked into only 1.3mm length by process, and reduce pressure using larger passage sectional dimension
Drop.
3. the present invention greatly reduces flow distance of the oil in microchannel in mixed process so that common fluid machinery
It is enough the flowing that oil phase is provided；And for aqueous phase, emulsifier unit of the invention devises less channel cross-section size, to
Enough kinetic energy is provided.Emulsifying effectiveness improves.
Brief description of the drawings
Fig. 1 is the side sectional view of the emulsifier unit of the present invention.
Fig. 2 is the Facad structure figure of the emulsifier unit of the present invention.
Reference
First fluid outlet 11；First fluid air deflector 12；First fluid passage 13；Second fluid outlet 21；Second
Body air deflector 22；Second fluid passage 23；Water conservancy diversion header 3.
Embodiment
Embodiments of the present invention are described with reference to the accompanying drawings, wherein identical part is presented with like reference characters.
In the case where not conflicting, the technical characteristic in following embodiment and embodiment can be mutually combined.
Fig. 1 shows the structure chart of the emulsifier unit of the present invention, and specifically, Fig. 1 is the sectional view of side.The present invention's
Emulsifier unit includes：For the first fluid passage 13 of high viscosity fluid, for the second fluid passage 23 of low viscosity fluid,
The fluid inlet end of one fluid passage 13 is connected to first fluid air deflector 12, the fluid inlet end connection of second fluid passage 23
To second fluid air deflector 22.The first fluid outlet 11 of first fluid passage 13 and the second fluid of second fluid passage 23 go out
Mouth 21 is commonly connected to water conservancy diversion header 3.Water conservancy diversion header 3 is located at the front end of emulsifier unit, first fluid air deflector 12 and second
Body air deflector 22 is located at the rear end of emulsifier unit.
Multiple first fluid passages 13 can be set (along Fig. 1 paper vertical direction) side by side, likewise, (edge side by side
Fig. 1 paper vertical direction) multiple second fluid passages 23 can be set.
Preferably, first fluid air deflector 12 is horn-like that one end of connection first fluid passage 13 is small.Second fluid is led
Device 22 is flowed to be horn-like, and one end of connection second fluid passage 23 is small.Because the first first fluid passage 13 and second fluid lead to
Small-sized (micron order) in road 23, first fluid air deflector 12, second fluid air deflector 22 can connect the thick of external fluid
Supply pipe (Centimeter Level) so that fluid can smooth water conservancy diversion.
Preferably, second fluid passage 23 is arc, high at second fluid outlet 21, at second fluid air deflector 22
It is low.It is that therefore, the space of the rear end of emulsifier unit is stayed in order to provide common fluid intake to high viscosity fluid to be designed as arc
To high viscosity oil phase as entrance.Purpose is to reduce pressure drop.Therefore, the rear end of emulsifier unit has not had space to place aqueous phase again
Entrance, therefore the entrance of aqueous phase is arranged below.Arcuate structure avoids the pressure drop of increase aqueous phase simultaneously.
Preferably, first fluid passage 13 is shorter than second fluid passage 23.For example, first fluid is oil, second fluid is
Water.When oily ratio of viscosities water used is much larger, the oily passage of design is shorter than aquaporin a lot, shortens oil by microchannel
Length, oily pressure drop are reduced seldom in the process, improve the utilization ratio of energy.In one embodiment, it is first-class
The length of body passage 13 is in the range of 1.2-1.5mm, can be 1.3 millimeters, if too short, the expansion of oil phase passage and aqueous phase passage
Scattered chained technology can not effectively realize link on the premise of micro-structural is not damaged.The width of first fluid passage 13 is 0.3 milli
Rice, is highly 0.2 millimeter.Emulsification test is carried out using the blender.Raw material is done using water and certain high viscosity fluid, it is Celsius 95
Degree, when Dang Shui and oil flow are respectively 5kg/h, the pressure drop of oil phase is only 0.5Bar, and the Suo Te for generating emulsion droplet is averagely straight
About 7 microns of footpath.
Preferably, hybrid chamber 31 is set in water conservancy diversion header 3, and first fluid outlet 11 and second fluid outlet 21 are led to mixed
Close in chamber 31, mixed behind two kinds of fluid outflow microchannels in hybrid chamber 31.
The emulsifier unit of the present invention farthest shortens the length of oil phase passage so that pressure is preferably minimized, but another
Aspect, which can not be short to, can not use Diffusion bonding techniques.Also, the wide high numerical value of channel cross-section reaches a compromise：Oil phase passage
It is small to avoid to the high mass transfer characteristic that embody microchannel while to a certain extent the high viscosity of oil phase to lose greatly.
Embodiment described above, it is the present invention more preferably embodiment, those skilled in the art is at this
The usual variations and alternatives carried out in the range of inventive technique scheme should all include within the scope of the present invention.
Claims (10)
- A kind of 1. emulsifier unit, it is characterised in that including：First fluid passage (13) for high viscosity fluid；Second fluid passage (23) for low viscosity fluid；First fluid air deflector (12), the fluid inlet end of first fluid passage (13) are connected to first fluid air deflector (12)；Second fluid air deflector (22), the fluid inlet end of second fluid passage (23) are connected to second fluid air deflector (22)；Water conservancy diversion header (3), the first fluid outlet (11) of first fluid passage (13) and the second of second fluid passage (23) Body outlet (21) is commonly connected to water conservancy diversion header (3).
- 2. emulsifier unit according to claim 1, it is characterised in that including：Second fluid passage (23) is arc, high at second fluid outlet (21) place, low at second fluid air deflector (22) place.
- 3. emulsifier unit according to claim 1, it is characterised in thatFirst fluid air deflector (12) is horn-like, and one end of connection first fluid passage (13) is small.
- 4. emulsifier unit according to claim 1, it is characterised in thatSecond fluid air deflector (22) is horn-like, and one end of connection second fluid passage (23) is small.
- 5. emulsifier unit according to claim 1, it is characterised in thatFirst fluid passage (13) is above second fluid passage (23).
- 6. emulsifier unit according to claim 1, it is characterised in thatThe length of first fluid passage (13) is in the range of 1.2-1.4 millimeters.
- 7. emulsifier unit according to claim 1, it is characterised in thatThe length of first fluid passage (13) is 1.3 millimeters, and width is 0.3 millimeter, is highly 0.2 millimeter.
- 8. emulsifier unit according to claim 1, it is characterised in thatFirst fluid passage (13) be arranged side by side it is multiple, second fluid passage (23) be arranged side by side it is multiple, outlet be all connected to institute State water conservancy diversion header (3).
- 9. emulsifier unit according to claim 1, it is characterised in thatThe outlet of multiple first fluid passages (13) is all connected to first fluid air deflector (12),The outlet of multiple second fluid passages (23) is all connected to second fluid air deflector (22).
- 10. emulsifier unit according to claim 1, it is characterised in that also include：Hybrid chamber (31), hybrid chamber (31) are located in water conservancy diversion header (3), first fluid outlet (11) and second fluid outlet (21) Lead in hybrid chamber (31), mixed after two kinds of fluid outlet passages in hybrid chamber (31).
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710825953.5A CN107519775A (en) | 2017-09-14 | 2017-09-14 | A kind of emulsifier unit |
| CN201820960835.5U CN208678849U (en) | 2017-09-14 | 2018-06-21 | A kind of emulsifier for heavy oil phase |
| CN201810645360.5A CN108889150B (en) | 2017-09-14 | 2018-06-21 | Emulsifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710825953.5A CN107519775A (en) | 2017-09-14 | 2017-09-14 | A kind of emulsifier unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107519775A true CN107519775A (en) | 2017-12-29 |
Family
ID=60735939
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710825953.5A Pending CN107519775A (en) | 2017-09-14 | 2017-09-14 | A kind of emulsifier unit |
| CN201810645360.5A Active CN108889150B (en) | 2017-09-14 | 2018-06-21 | Emulsifying device |
| CN201820960835.5U Active CN208678849U (en) | 2017-09-14 | 2018-06-21 | A kind of emulsifier for heavy oil phase |
Family Applications After (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810645360.5A Active CN108889150B (en) | 2017-09-14 | 2018-06-21 | Emulsifying device |
| CN201820960835.5U Active CN208678849U (en) | 2017-09-14 | 2018-06-21 | A kind of emulsifier for heavy oil phase |
Country Status (1)
| Country | Link |
|---|---|
| CN (3) | CN107519775A (en) |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11347392A (en) * | 1998-06-11 | 1999-12-21 | Hitachi Ltd | Stirrer |
| US7918244B2 (en) * | 2005-05-02 | 2011-04-05 | Massachusetts Institute Of Technology | Microfluidic bubble logic devices |
| DE102005034642B3 (en) * | 2005-07-25 | 2006-08-03 | Siemens Ag | Laboratory microfluidic analytical mixer unit has two separate passage systems, one of which has internal leak detector |
| JP2008100182A (en) * | 2006-10-20 | 2008-05-01 | Hitachi Plant Technologies Ltd | Emulsification apparatus and apparatus for manufacturing particulate |
| CN201421455Y (en) * | 2008-12-30 | 2010-03-10 | 宁波大学 | Special micro-fluidic chip for syphilis diagnosis |
| KR101309524B1 (en) * | 2011-04-28 | 2013-10-15 | 가천대학교 산학협력단 | Method for Detecting DNA Using Microfluidic Reactor |
| CN102500256A (en) * | 2011-11-11 | 2012-06-20 | 南通申东冶金机械有限公司 | Rotary jet mixer |
| SG11201501837TA (en) * | 2012-09-21 | 2015-04-29 | Massachusetts Inst Technology | Micro-fluidic device and uses thereof |
-
2017
- 2017-09-14 CN CN201710825953.5A patent/CN107519775A/en active Pending
-
2018
- 2018-06-21 CN CN201810645360.5A patent/CN108889150B/en active Active
- 2018-06-21 CN CN201820960835.5U patent/CN208678849U/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN108889150A (en) | 2018-11-27 |
| CN208678849U (en) | 2019-04-02 |
| CN108889150B (en) | 2023-04-18 |
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| PB01 | Publication | ||
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| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20171229 |